Ce3+复合聚合硫酸铁絮凝剂的光谱分析及处理油田废水性能研究

以FeSO.47H2O为原料,NaClO3氧化法制备出聚合硫酸铁,并用Ce3+与其进行复合得到复合絮凝剂.运用紫外光谱及傅里叶红外光谱对絮凝剂样品进行了表征,并通过CODCr去除率和浊度去除率考察了絮凝剂处理油田废水的性能.结果表明,Ce3+与聚合硫酸铁复合以后,Ce3+与聚合硫酸铁中的羟基作用形成了新的化学键Ce—OH—Fe,实现了Ce3+与聚合硫酸铁的成功复合.该复合絮凝剂对油田废水的处理效果均优于聚合硫酸铁,当复合比为1.5%时处理效果最好,CODC r去除率和浊度去除率均接近或高于90%,表现出良好的应用前景.     

改性沸石及添加CaCl2和MgCl2对重金属离子Pb2+吸附特性的影响

研究天然沸石和改性沸石对Pb2+吸附的性能,探讨不同因素对沸石吸附Pb2+的影响.结果表明,天然沸石经过3种不同方法改性后均可促进其对Pb2+的吸附.氢氧化钠改性沸石吸附Pb2+效果最好,其次是硝酸钾改性沸石,氯化铵改性沸石吸附Pb2+效果稍差一些.不同Pb2+初始浓度、沸石使用量、pH和温度均对天然沸石和改性沸石吸附Pb2+有影响.天然沸石和改性沸石对Pb2+的等温吸附可用Langmuir方程和Freundlich方程来拟合,其中Langmuir方程的拟合效果较好,相关系数在0.9203—0.9840之间.CaCl2和MgCl2可影响天然沸石和改性沸石对Pb2+的吸附.当CaCl2和MgCl2的浓度均为10 mmol.L-1时,天然沸石吸附Pb2+量分别比对照处理提高66.6%和54.5%.添加2—10 mmol.L-1CaCl2和MgCl2导致氯化铵改性沸石吸附Pb2+分别比对照处理提高16.4%—18.8%和16.8%—19.9%.研究结果表明,采用沸石去除废水中的Pb元素时必须考虑不同因素的影响,以达到重金属去除效率的最大化.     

不同作物原料热裂解生物质炭对溶液中Cd2+和Pb2+的吸附特性

选择由小麦秸秆、玉米秸秆和花生壳经350~500℃热裂解制成的生物质炭,研究生物黑炭对水溶液中Cd2+和Pb2+的吸附特性,分析了pH值、吸附时间、溶液初始质量浓度、生物质炭粒径和投加量对吸附效果的影响。结果表明:生物质炭对Cd2+和Pb2+的吸附约10 min即达平衡;3种生物质炭对Cd2+和Pb2+的等温吸附均可用Langmuir方程和Freundlich方程拟合,玉米秸秆炭对Cd2+和Pb2+的最大吸附量远大于小麦秸秆炭和花生壳炭;在生物黑炭投加量为150 mg(6 g.L-1)时,3种生物黑炭对溶液Cd2+的去除率均在90%以上,玉米秸秆炭对溶液Pb2+的去除率达90.30%,而小麦秸秆炭和花生壳炭的去除率仅为52%和47%,玉米秸秆炭有望成为处理重金属污染废水的新型吸附材料。     

离子强度对恒电荷土壤胶体吸附Cu2+和Pb2+的影响

采用平衡法研究了离子强度、表面电位对恒电荷土壤胶体吸附Cu2+和Pb2+的影响.结果表明,离子强度越小,表面电位越高,土壤胶体对Cu2+和Pb2+的吸附量越大.在离子强度小于1.0mol*kg-1范围内,土壤胶体对Cu2+和Pb2+的吸附包括静电吸附和专性吸附;离子强度大于1.0mol*kg-1以后,土壤胶体对Cu2+和Pb2+的吸附受专性吸附控制.     

微波辅助HNO3改性竹炭对Cu2+的吸附性能

以竹炭为原料,采用HNO3(NA)作为改性药剂,通过微波辅助加热的方法对竹炭进行改性;运用Boehm滴定、扫描电子显微镜(SEM)、电子能谱(EDAX)和红外光谱(FTIR)对改性竹炭进行了表征;考察了pH、时间、温度和离子强度等对改性竹炭吸附Cu2+的影响.研究结果表明,微波辅助硝酸改性使得竹炭表面的羧基、酚羟基、内酯基等酸性含氧官能团的数量有所增加;改性竹炭对Cu2+吸附更符合Langmuir等温方程,吸附为自发的吸热过程;吸附动力学符合准二级动力学方程;溶液离子强度增大不利于其对Cu2+的吸附.     

硅酸钙吸附法预处理焦化废水中COD和NH3-N

焦化废水是一种典型的含有高污染、难降解有机物的高浓度工业废水,生物处理是目前处理焦化废水的核心技术.由于焦化废水高浓度污染物对微生物活性产生抑制作用,经生物处理后其COD及NH3-N等指标仍很难达标.因此,在进入生物处理系统前往往采用物理法或化学法对焦化废水进行预处理,使氰化物、COD及NH3-N等难降解物指标得到一定程度的降低,为后续生物处理降低负荷.     

磷酸活化活性炭对Cu2+的吸附特征研究

寻求廉价而高效的吸附材料为目的,研究向日葵秸杆基活性炭对铜离子的吸附性能。以向日葵秸秆为原料,经H3PO4活化制备活性炭,通过静态实验研究了其对水溶液中Cu2+的吸附特性,考察了溶液pH值、吸附温度和离子强度对吸附的影响,探讨了吸附热力学、动力学和吸附机理。结果表明:溶液pH值为5～6时活性炭对Cu2+的去除效果最好;向50 mL 170 mg·L-1的溶液中加入0.5 g活性炭,温度为45℃、吸附时间为1 h时,对Cu2+的去除率可达98.3%;Langmuir方程能更好地描述Cu2+在活性炭上的等温吸附特征,静态吸附容量可达41.03 mg·g-1;吸附过程符合拟二级动力学过程,且为吸热的化学吸附过程,膜扩散为速率控制步骤,离子交换可能在吸附过程中起了重要作用。     

以NH2-MIL-53(Al)为前驱体制备多孔掺碳Al2O3吸附剂及其对水中Cr(Ⅵ)的吸附性能

铬是污染性金属元素,铬含量是水质污染控制的一项重要指标,其中Cr(Ⅵ)的毒性最大,且易被人体吸收.本研究以水中的Cr(Ⅵ)吸附传质分离为目标,利用以铝为金属源水热法合成的铝基MOFs为前驱体,600℃煅烧后制备了多孔掺碳Al₂O₃吸附材料,利用现代分析技术对其进行微观结构表征,探究了其吸附作用能力与机制.研究结果表明,XRD、SEM、BET等表征手段证明了NH₂-MIL-53(Al)与多孔掺碳Al₂O₃结构的成功合成.前驱体NH₂-MIL-53(Al)和煅烧后的衍生物多孔掺碳Al₂O₃,在形貌上相似,且多孔掺碳Al₂O₃材料(180.24 m²·g^-1)的比表面积要大于NH₂-MIL-53(Al)(116.73 m²·g^-1).多孔掺碳Al₂     

硫酸盐废水生物处理产生的硫化物处理含Pb2+、Zn2+的钢丝酸洗废水

在一套小型搅拌反应器中,研究了碱沉淀(KOH,处理a)、碱沉淀及硫酸盐废水厌氧处理产生的硫化物出水混合(KOH+出水混合,处理b)、碱沉淀及N2吹脱硫酸盐废水厌氧处理产生的硫化物(KOH+N2吹脱,处理c),以及碱沉淀、硫酸盐废水厌氧处理产生的硫化物出水混合和N2吹脱硫化物联合(KOH+出水混合+N2吹脱,处理d)等4组处理方式对含Zn2+、Pb2+的钢丝绳酸洗废水处理效果的影响.废水pH值为0.7,Zn2+和Pb2+含量分别为450和3274 mg.L-1.结果表明,KOH+出水混合+N2吹脱的处理方式对废水有较好的处理效果,Zn2+和Pb2+的去除为氢氧化物、硫化物沉淀的共同作用结果,处理后,废水中Zn2+和Pb2+的去除率均达99.6%以上,满足污水综合排放标准(GB 8978—1996).     

纳米水稳型C60（nC60）促进Zn2+和Cr6+ 在大型溞体内的吸收、抗氧化性和急性毒性

富勒烯(C60)作为一种被广泛使用的纳米工程材料,其环境行为和所造成的毒效应越来越引起人们的关注,特别是其与重金属的联合毒性.文章选取模式生物大型溞研究纳米水稳型富勒烯(nC60)与Zn+和Cr6+的联合毒性.按EPA 2024急性毒性试验结果,nC60对大型溞48 h-LC50为0.47 mg·L-1,最大无观察效应浓度(NOEC)为0.10 mg·L-1.NOEC浓度选定为nC60亚急性试验浓度,用于联合毒性试验.nC60增强了Zn2+和Cr6+对大型溞的毒性,Zn2和Cr6+对大型溞48 h-LC50分别由2.33mg·L-1和0.40mg·L-1降低为1.52 mg·L-1和033 mg·L-1;nC60增加了大型溞对Zn2+和Cr6+的摄入,暴露1440 min后体内Zn2+和Cr6+累积量分别由6.52 μg·g-1湿重和1.52 μg·g-1湿重增加到9.98 μg ·g-1湿重和3.01 μg·g-1湿重;nC60和Zn2+和Cr6+联合作用于大型潘后,大型溞SOD酶活性均呈现出增强的诱导现象,联合作用时诱导作用强于两种物质单独作用.此研究表明:在亚急性浓度下,nC60增强了Zn2+和Cr6+对大型溞的毒性,提高了大型潘体内Zn2+和Cr6+的积累,并提高大型溞体内自由基活性.     

Effective removal of Cd2+ and Pb2+ pollutants from wastewater by dielectrophoresis-assisted adsorption

Dielectrophoresis (DEP) process could enhance the removal the Cd²⁺ and Pb²⁺ with less absorbent. The removal rates of both Cd²⁺ and Pb²⁺ increased with the increase of voltage. The overall removal rate of Cd²⁺ and Pb²⁺ in the binary system is higher than that of Cd²⁺ or Pb²⁺ in the single system. DEP could cause considerable changes of the bentonite particles in both surface morphology and microstructure. Dielectrophoresis (DEP) was combined with adsorption (ADS) to simultaneously and effectively remove Cd²⁺ and Pb²⁺ species from aqueous solution. To implement the process, bentonite particles of submicro-meter size were used to first adsorb the heavy metal ions. These particles were subsequently trapped and removed by DEP. The effects of the adsorbent dosage, DEP cell voltage and the capture pool numbers on the removal rate were investigated in batch processes, which allowed us to determine the optimal experimental conditions. The high removal efficiency, 97.3% and 99.9% for Cd²⁺ and Pb²⁺, respectively, were achieved when the ions are coexisting in the system. The microstructure of bentonite particles before and after ADS/DEP was examined by scanning electron microscopy. Our results suggest that the dielectrophoresis-assisted adsorption method has a high capability to remove the heavy metals from wastewater.     

Selective recovery of Cu2+ and Ni2+ from wastewater using bioelectrochemical system

As the bioelectrochemical system, the microbial fuel cell (MFC) and the microbial electrolysis cell (MEC) were developed to selectively recover Cu²⁺ and Ni²⁺ ions from wastewater. The wastewater was treated in the cathode chambers of the system, in which Cu²⁺ and Ni²⁺ ions were removed by using the MFC and the MEC, respectively. At an initial Cu²⁺ concentration of 500 mg·L^-1, removal efficiencies of Cu²⁺ increased from 97.0%±1.8% to 99.0%±0.3% with the initial Ni²⁺ concentrations from 250 to 1000 mg·L^-1, and maximum power densities increased from 3.1±0.5 to 5.4±0.6 W·m^-3. The Ni²⁺ removal mass in the MEC increased from 6.8±0.2 to 20.5±1.5 mg with the increase of Ni²⁺ concentrations. At an initial Ni²⁺ concentration of 500 mg·L^-1, Cu²⁺ removal efficiencies decreased from 99.1%±0.3% to 74.2%±3.8% with the initial Cu²⁺ concentrations from 250 to 1000 mg·L^-1, and maximum power densities increased from 3.0±0.1 to 6.3±1.2 W·m^-3. Subsequently, the Ni²⁺ removal efficiencies decreased from 96.9%±3.1% to 73.3%±5.4%. The results clearly demonstrated the feasibility of selective recovery of Cu²⁺ and Ni²⁺ from the wastewater using the bioelectrochemical system.     

Cu~(2+)、Zn~(2+)、Cd~(2+)、Cr~(6+)和Mn~(2+)对萼花臂尾轮虫联合急性毒性研究

为探究重金属复合污染对轮虫的毒性影响,以萼花臂尾轮虫为受试动物,选择Cu~(2+)、Zn~(2+)、Cd~(2+)、Cr6+和Mn~(2+)等5种重金属,采用水生毒理联合效应相加指数法开展了其24 h联合急性毒性作用的评价研究。结果显示,Cu~(2+)、Zn~(2+)、Cd~(2+)、Cr6+和Mn~(2+)等5种重金属对萼花臂尾轮虫24 h半数致死浓度分别为:0.00616 mg·L~(-1),12.62 mg·L-1,2.89 mg·L-1,17.29 mg·L-1和67.32 mg·L-1。联合急性毒性实验结果显示,等毒性配比的Cu~(2+)-Cr6+(0.00385-10.806 mg·L-1)和等浓度配比的Cu~(2+)-Zn~(2+)(0.0199-0.0199 mg·L-1)、Cu~(2+)-Cd~(2+)(0.0181-0.0181 mg·L-1)、Cu~(2+)-Cr6+(0.0118-0.0118 mg·L~(-1))、Zn~(2+)-Cd~(2+)(3.475-3.475 mg·L-1)二元联合测试液的作用结果显示为拮抗效应,其余二元联合测试液的作用结果则均显示是协同效应。等毒性配比的Cu~(2+)-Cr~(6+)-Mn~(2+)(0.00210-5.902-22.981 mg·L-1)和等浓度配比的Cu~(2+)-Cd~(2+)-Mn~(2+)(0.00727-0.00727-0.00727 mg·L-1)三元联合测试液的作用结果显示为拮抗效应,其余三元联合测试液的作用结果则均显示是协同效应。等浓度配比的Cu~(2+)-Zn~(2+)-Cd~(2+)-Cr6+(0.00907-0.00907-0.00907-0.00907 mg·L-1)、Cu~(2+)-Zn~(2+)-Cd~(2+)-Mn~(2+)(0.00898-0.00898-0.00898-0.00898 mg·L~(-1))、Cu~(2+)-Zn~(2+)-Cr6+-Mn~(2+)(0.00819-0.00819-0.00819-0.00819 mg·L~(-1))四元联合测试液的作用结果显示为拮抗效应,其余四元联合测试液的作用结果的则均显示是协同效应。Cu~(2+)-Zn~(2+)-Cd~(2+)-Cr~(6+)-Mn~(2+)等毒性(0.00074-1.520-0.348-2.082-8.107 mg·L~(-1))和等浓度(0.00582-0.00582-0.00582-0.00582-0.00582 mg·L-1)配比的五元联合测试液作用结果均显示是协同效应。     

Cu2+、Cd2+和Cr6+对斑马鱼联合毒性作用和生物预警的研究

为了研究重金属对水生生物的联合毒性作用,以斑马鱼为受试生物,采用半静态法,在研究Cu2、Cd2和Cr6+对斑马鱼单一毒性的基础上,以获得的Cu2+、Cd2+和Cr6+的96 h-LC50数据,利用等效应曲线法研究了Cu-Cd、Cu-Cr和Cd-Cr的联合毒性作用,并综合分析环境毒理学指标的测定结果,考察利用斑马鱼作为水...     

Cr~(3+)胁迫对小球藻生理生化特性的影响

水体重金属污染较难处理,且会对水生物造成严重的影响。为探讨水体中重金属对藻类的毒性影响,以普通小球藻(Chlorella vulgaris)和铬(Cr~(3+))为材料,研究不同浓度Cr~(3+)对普通小球藻生理、生化特性的影响,检测不同浓度的Cr~(3+)对小球藻的毒性效应。结果表明,小球藻的最优生长温度为31℃。此条件下,Cr~(3+)浓度为3 mg·L~(-1)时,小球藻的生物量最大。Cr~(3+)的浓度低于3 mg·L~(-1)时,Cr~(3+)能促进小球藻的生长,且藻细胞中光合色素、蛋白质、可溶性糖、丙二醛(MDA)的含量及超氧化物歧化酶(SOD)的活性也逐渐增加。当各胁迫组的Cr~(3+)浓度超过3 mg·L~(-1)时,随着Cr~(3+)浓度的提高,C.vulgaris的生长受到明显的抑制,藻细胞的光合色素、蛋白质和可溶性糖含量呈现逐渐下降的趋势,而MDA含量持续增加,SOD和脯氨酸则表现出先持续增高后降低(Cr~(3+)浓度为7 mg·L~(-1)时)的趋势。证明不同浓度的Cr~(3+)对小球藻的生理生化特性有不同程度的毒性效应。     

Immobilization of Cu2+, Zn2+, Pb2+, and Cd2+ during geopolymerization

The present research explored the application of geopolymerization for the immobilization and solidification of heavy metal added into metakaolinte. The compressive strength of geopolymers was controlled by the dosage of heavy metal cations, and geopolymers have a toleration limit for heavy metals. The influence of alkaline activator dosage and type on the heavy metal ion immobilization efficiency of metakaolinte-based geopolymer was investigated. A geopolymer with the highest heavy metal immobilization efficiency was identified to occur at an intermediate Na₂SiO₃ dosage and the metal immobilization efficiency showed an orderly increase with the increasing Na⁺ dosage. Geopolymers with and without heavy metals were analyzed by the X-ray powder diffraction (XRD) and Fourier transform infrared (FTIR) spectroscopy. No crystalline phase containing heavy metals was detected in geopolymers with heavy metal, suggesting that the crystalline phase containing heavy metals is not produced or most of the phases incorporating heavy metals are amorphous. FTIR spectroscopy showed that, with increasing heavy metal addition, an increase in NO3- peak intensity was observed, which was accompanied by a decrease in the CO32- peak.     

硅藻土和膨润土对重金属离子Zn~（2＋）、Pb~（2＋）及Cd~（2＋）的吸附特性

以硅藻土和膨润土作为吸附剂,考察微波加热与否条件下,不同吸附时间、不同吸附剂用量和不同pH值对硅藻土和膨润土分别吸附Zn2＋、Pb2＋、Cd2＋重金属离子的影响.实验结果表明,硅藻土和膨润土对3种重金属离子均有很好的吸附效果,吸附时间对去除率影响不大,数分钟即可达到吸附平衡,微波加热、增加吸附剂用量和提高pH值,都有利于提高3种重金属离子的去除率.     

Preparation of amphiphilic composite and removal of oil and hexavalent chromium from wastewater

A new composite for water treatment was prepared by melt blend for oil and hexavalent chromium absorption. Ethylene Propylene Diene Monomer (EPDM) was the matrix, calcinatory Fe₂O₃ and anion-exchange resin 201×7 were the fillers. This composite can suspend in water–oil contact (WOC) and absorb oils and hexavalent chromium in wastewater simultaneously. The absorbencies of composites changed greatly with various ratios of calcinatory Fe₂O₃ and anion-exchange resin 201×7. The results showed that the oil absorbencies increased continuously and hexavalent chromium absorbencies were step-down as calcinatory Fe₂O₃ loadings from 13 to 19%. The composite can adsorb oils and hexavalent chromium simultaneously. The optimized proportion of calcinatory Fe₂O₃ and anion-exchange resin 201×7 in composite was found when the absorbencies of oils and hexavalent chromium reaching the maximum simultaneously. This composite is an inexpensive, convenient and high efficiency material for removing oils and hexavalent chromium from wastewater.